Producing method of phospholipids including long-chain polyunsaturated fatty acids as constituents, and use of such phospholipids

ABSTRACT

The present invention provides a method of efficiently and stably producing LCPUFA-PL. Specifically, the invention provides a method for producing phospholipids that contain LCPUFA as a constituent (LCPUFA-PL), wherein lipid producing cells producing lipids that contain long-chain polyunsaturated fatty acids (LCPUFA) are used as a starting material, the method including a PL extracting step of extracting phospholipids (PL) from defatted cells obtained by extracting triglyceride (TG)-containing oil or fat from the lipid producing cells.

CROSS REFERENCE TO RELATED APPLICATIONS

This application is a continuation of application Ser. No. 10/591,329,filed Jun. 14, 2007, which is a National Stage of InternationalApplication No. PCT/JP2005/003344, filed Feb. 28, 2005, which claims thebenefit of Japanese Patent Application No. 2004-056928, filed Mar. 1,2004, and which are incorporated by reference herein in their entirety.

TECHNICAL FIELD

The present invention relates to a producing method of phospholipidsincluding long-chain polyunsaturated fatty acids as constituents, anduse of such phospholipids. The invention particularly relates to amethod for efficiently and stably producing phospholipids, and tophospholipids produced by the method, and representative use of suchphospholipids.

BACKGROUND ART

Phospholipids (PL) are known to possess various physiological functions,including brain function improving effect, anti-stress effect, andcholesterol reducing action. PL occur in various forms, well-knownexamples of which include phosphatidylcholine (PC), phosphatidylserine(PS), phosphatidylethanolamine (PE), and phosphatidylinositol (PI).These different forms of PL have different functions and properties.

Among these different types of PL, phospholipids whose constituents arelong-chain polyunsaturated fatty acids (may be referred to as “LCPUFA”hereinafter) with 20 or greater carbon atoms (may be referred to as“LCPUFA-PL” for convenience of explanation) are known to exhibitsuperior brain function improving effect, as compared with phospholipidswhose constituents are not LCPUFA (may be referred to as “non-LCPUFA-PL”for convenience of explanation) (see Non-Patent Publication 1, forexample). Specific examples of LCPUFA include, for example,docosahexaenoic acid (DHA), arachidonic acid (AA) and the like.

Non-phospholipid LCPUFA derivatives are also known to possess brainfunction improving effects (see Patent Publication 1, for example).However, unlike phospholipids such as the LCPUFA-PL or Non-LCPUFA-PL,the non-phospholipid LCPUFA derivatives are believed to act on thehippocampus of the cerebrum to improve the brain functions.

The LCPUFA-PL is considered to provide superior brain function improvingeffect because (1) it has the structure actually present in the brain,(2) it can pass through the blood brain barrier, and (3) it can reachthe brain tissue or other tissues in the body without being captured ormodified in the liver, since the molecule is absorbed without enteringthe liver.

The following more specifically describes these reasons. (1) The LCPUFAin the brain is known to exist almost entirely in the form ofphospholipids. More specifically, most of LCPUFA exist as compounds suchas PC, PS, PE, and PI, and therefore exhibit a variety of functions inthe brain. (2) The phospholipids can reach the brain tissue. This hasbeen proved by an experiment in which orally administeredlabeled-phospholipids were detected in the brain tissue (see Non-PatentPublication 2). (3) When absorbed, one of the two fatty acid moleculesof the phospholipids is hydrolyzed to generate lysophospholipids in thedigestive system. The lysophospholipids are absorbed in the smallintestine and reassembled into phospholipids in the small intestinecells before they are absorbed through the lymph vessels (Non-PatentPublication 3). In this manner, the LCPUFA-PL circulates through thebody without entering the liver.

Conventionally, the LCPUFA-PL has been produced by being prepared orpurified from organs, eggs, or other parts of animals containing a largeamount of LCPUFC-PL. In one specific example, the LCPUFA-PL is preparedfrom the cow brain, or a phospholipid fraction from the pig liver orfish egg is purified (see Patent Publications 2 and 3). Further,particular species of marine bacteria are known to produce LCPUFA-PL(see Non-Patent Publication 4). Furthermore, it is also known thatarachidonic acid-producing filamentous bacteria produce a small amountof phospholipids containing arachidonic acid in addition to a largeamount of triglycerides containing arachidonic acid (see Non-PatentPublication 5).

In the industrial production of phospholipids, phospholipids aregenerally extracted together with oil or fat, when the oil or fat, ofwhich primary ingredient are triglycerides, is extracted from a startingmaterial. Hexane or the like solvent is used as a solvent forextraction.

The extracted oil or fat includes gum substance, which may cause thecoloring and foaming of the oil or fat. Therefore the gum substance isremoved through a gum-removing process, in which almost all parts ofphospholipids are transferred to the gum substance. Accordingly,phospholipids are produced by purification of the gum substance.

In the case where soy bean lecithin is produced as phospholipids, rawoil is extracted from soy, which is a starting material in this case, byusing hexane as a solvent. The residual defatted soy is used as food,feedstuff or the like. As the raw oil, on the other hand, includes gumsubstance, the gum substance is separated through a gum-removing processand then purified. Through the process the soy bean lecithin isproduced. When the content of the soy bean lecithin or phospholipids isdetected after the aforementioned series of production steps of the soybean lecithin, from 1.5% to 2.5% of phospholipids is contained in theraw oil indeed, but the content of phospholipids in the purified oil isno more than 0.05%. Consequently, it becomes apparent that thephospholipids are removed mainly through gum-removing process (seeNon-Patent Publication 6).

[Patent Publication 1]

-   Japanese Laid-Open Patent Publication No. 48831/2003 (Tokukai    2003-48831) (published on Feb. 21, 2003)

[Patent Publication 2]

-   Japanese Laid-Open Patent Publication No. 35587/1999 (Tokukaihei    11-35587) (Published on Feb. 9, 1999)

[Patent Publication 3]

-   Japanese Laid-Open Patent Publication No. 59678/1996 (Tokukaihei    08-59678) (Published on Mar. 5, 1996)

[Non-Patent Publication 1]

-   G. Toffano et al., Nature Vol. 260 p 331-333 (1976)

[Non-Patent Publication 2]

-   G. Toffano et al. Clinical Trial Journal Vol. 24 p 18-24 (1987)

[Non-Patent Publication 3]

-   Katsumi Imaizumi, Clinical Nutrition (Rinsho Eiyo), Vol. 67, p. 119    (1985)

[Non-Patent Publication 4]

-   Kazunaga Yazawa et al., Oil Science (Abura Kagaku), Vol. 44, pp.    787-793 (1995)

[Non-Patent Publication 5]

-   S. jareonkitmongkol et al., Apple Environ Microbiol Vol. 59 p    4300-4304 (1993)

[Non-Patent Publication 6]

-   Oils and Fats Handbook, Saiwai Shobou, p. 178-184 (1988)

But through the conventional techniques, it is difficult to produceLCPUFA-PL efficiently and stably.

Specifically, sources of LCPUFA-PL are limited and only a small amountof LCPUFA-PL can be obtained because the LCPUFA-PL currently availableall derive from the aforementioned animal organs, or the egg yolk ofanimals. The supply is therefore unstable, and the same quality cannotalways be obtained. Further, with the epidemic of the mad-cow disease,it has become very difficult to use the cow brain or other animalorgans.

As for the technique using microbe, in the LCPUFA-PL derived from marinebacteria, the majority of its fatty acids are branched fatty acids whichare distinct to bacteria and are rarely seen in humans or other animals.The LCPUFC-PL derived from marine bacteria is therefore not suitable asa nutritional composition for human consumption. Further, thougharachidonic acid-producing filamentous bacteria produce phospholipidscontaining arachidonic acid, only a small amount is detected in amixture of a large amount of triglycerides. Therefore it is difficult toapply this method in an industrial application.

The present invention was made in view of the foregoing problems. Anobject of the invention is to provide a technique to produce LCPUFA-PLefficiently and stably, and to provide low-cost LCPUFA-PL with a stablequality in stable quantity. Another object of the invention is toprovide representative application of the technique.

DISCLOSURE OF INVENTION

The inventors of the present invention diligently worked to solve theforegoing problems. In accomplishing the present invention, thefollowing findings (1) and (2) were obtained when lipid producing cellsthat produce LCPUFA lipids were used as a starting material to produceLCPUFA-PL. (1) In extracting triglycerides from cells, the fraction ofthe extract containing triglycerides as a major component containedhardly any phospholipids, contrary to an expected outcome of findingphospholipids with the triglycerides. In the residual cells obtained bythe extraction of the triglycerides, a large amount of LCPUFA-PLremained. (2) From the defatted cells, it was possible to easily extractLCPUFA-PL with a simple procedure using an extractant such as an organicsolvent.

That is, the present invention provides a method for producingphospholipids that contain LCPUFA as a constituent (LCPUFA-PL), whereinlipid producing cells producing lipids that contain long-chainpolyunsaturated fatty acids (LCPUFA) are used as a starting material,the method including a PL extracting step of extracting phospholipids(PL) from defatted cells obtained by extracting triglyceride(TG)-containing oil or fat from the lipid producing cells.

It is preferable that the producing method further include an oil or fatextracting step of extracting TG-containing oil or fat from the lipidproducing cells and obtaining the defatted cells, the oil or fatextracting step being carried out before the PL extracting step.

The lipid producing cells used in the invention are not particularlylimited, but are preferably at least one kind selected from the groupconsisting of: Mortierella; Conidiobolus; Pythium; Phytophthora;Penicillium; Cladosporium; Mucor; Fusarium; Aspergillus; Rhodotorula;Entomophthora; Echinosporangium; and Saprolegnia. It is preferable thatthe lipid producing cells that belong to genus Mortierella also belongas subgenus Mortierella, and that the cells that belong to subgenusMortierella are Mortierella alpina.

It is preferable in the producing method that, in the PL extractingstep, an extract of at least one of an aliphatic organic solvent andwater, or supercritical carbon dioxide gas be used as an extractant usedto extract PL from the defatted cells. The aliphatic organic solvent ispreferably a saturated hydrocarbon, an alcohol, a mixed solvent ofsaturated hydrocarbon and alcohol, or a mixed solvent of halogenatedhydrocarbon and alcohol. It is preferable that the extract be at leastone of hexane, ethanol, methanol, hydrous ethanol, isopropyl alcohol,and acetone, and that the extract be a mixed solvent of hexane andethanol. A hexane:ethanol ratio of the mixed solvent of hexane andethanol is preferably in a range of 4:1 to 0:6 by volume.

It is preferable in the producing method that, in the oil or fatextracting step, the oil or fat be extracted from the lipid producingcells using at least one of compression extraction employing appliedpressure, rendering extraction, and extraction using an extractant. Itis preferable that an extract of at least one of an aliphatic organicsolvent and water, or supercritical carbon dioxide gas be used as theextractant used to extract PL from the defatted cells. Hexane ispreferably used as the aliphatic organic solvent. Preferably, the lipidproducing cells used in the oil or fat extracting step are dried cells.

Phospholipids according to the present invention are produced by theforegoing producing method, and include LCPUFA as a constituent. Theconstituent LCPUFA is not particularly limited, but is preferably atleast one kind selected from the group consisting of: eicosadienoicacid, eicosatrienoic acid, eicosatetraenoic acid, eicosapentaenoic acid,docosadienoic acid, docosatrienoic acid, docosatetraenoic acid,docosapentaenoic acid, docosahexaenoic acid, tetracosadienoic acid,tetracosatrienoic acid, tetracosatetraenoic acid, tetracosapentaenoicacid, and tetracosahexaenoic acid.

At least one of C—C double bonds in a LCPUFA molecule may be conjugated,and the LCPUFA preferably includes arachidonic acid and/ordocosahexaenoic acid. It is preferable that a proportion of arachidonicacid with respect to total fatty acids contained as constituents oftotal LCPUFA-PL is 5 percent by weight or greater.

Specifically, the LCPUFA-PL is preferably at least one kind ofglycerophospholipid selected from the group consisting of:phosphatidylcholine; phosphatidylserine; phosphatidylethanolamine;phosphatidylinositol; phosphatidic acid; and cardiolipin. In the casewhere the LCPUFA-PL is at least phosphatidylcholine, it is preferablethat a proportion of arachidonic acid with respect to total fatty acidscontained as constituents of total phosphatidylcholine be 15 percent byweight or greater. In the case where the LCPUFA-PL is at leastphosphatidylserine, it is preferable that a proportion of arachidonicacid with respect to total fatty acids contained as constituents oftotal phosphatidylserine be 20 percent by weight or greater.

In Phospholipids according to the present invention, the LCPUFA-PLincludes at least phosphatidylcholine and phosphatidylserine, and theLCPUFA includes at least arachidonic acid, and a proportion ofarachidonic acid with respect to total fatty acids contained asconstituents of total phosphatidylcholine is 40 percent by weight orgreater, and a proportion of arachidonic acid with respect to totalfatty acids contained as constituents of total phosphatidylserine is 20percent by weight or greater.

The phospholipids may be adapted so that the LCPUFA-PL includesphosphatidylcholine that at least includes dihomo-γ-linolenic acid asLCPUFA, and that a proportion of dihomo-γ-linolenic acid with respect tototal fatty acids contained as constituents of total phosphatidylcholineis 3 percent by weight or greater. Further, the phospholipids may beadapted so that the LCPUFA-PL includes phosphatidylserine that at leastincludes dihomo-γ-linolenic acid as LCPUFA, and that a proportion ofdihomo-γ-linolenic acid with respect to total fatty acids contained asconstituents of total phosphatidylserine is 1 percent by weight orgreater.

A method of producing a lipid composition according to the presentinvention includes: a PL extracting step of the foregoing producingmethod; and a solution preparing step of preparing a phospholipidsolution by dissolving the LCPUFA-PL-containing PL obtained in the PLextracting step in a liquid lipid that contain LCPUFA as a constituent.

It is preferable that the producing method further include an oil or fatextracting step, wherein oil or fat obtained in the oil or fatextracting step is used as the liquid lipid, and that an amount of oilor fat extracted in the oil or fat extracting step be suppressed, so asto extract in the PL extracting step the LCPUFA-PL as a lipidcomposition dissolved in the liquid lipid.

A lipid composition according to the present invention is produced bythe method of producing a lipid composition, and at least includes:LCPUFA-PL; and a liquid lipid including LCPUFA as a constituent. It ispreferable in the lipid composition that a proportion of LCPUFA withrespect to total fatty acids of the liquid lipid be 11 percent by weightor greater.

A lipid composition according to the present invention is notnecessarily required to be obtained by the method of producing a lipidcomposition as long as it contains the phospholipids.

A lipid composition according to the present invention may be used as anutritional composition, and may be processed into a capsule or tablet,for example.

In the present invention, the lipid composition may be used in food.That is, the present invention includes food that contains the lipidcomposition. Further, in the present invention, food may include anoil-in-water dispersion liquid in the form of a liposome formed by thephospholipids. A specific example of food is a nutriment.

For a fuller understanding of the nature and advantages of theinvention, reference should be made to the ensuing detailed description.

BEST MODE FOR CARRYING OUT THE INVENTION

The following will describe one embodiment of the present invention indetail. It should be noted that the invention is not limited in any wayby the following descriptions. Specifically, the present embodimentdescribes phospholipids and a producing method thereof, lipidcomposition and a producing method thereof, and use of the invention, inorder of appearance.

(I) Phospholipids According to the Invention, and a Producing MethodThereof

The present invention provides phospholipids that include LCPUFA asconstituents (LCPUFA-PL), using, as a starting material, lipid producingcells that produce lipids whose constituents are LCPUFA. The inventionalso provides a producing method of phospholipids (referred to simply asa “producing method” where appropriate), in which LCPUFA-PL is produced.Specifically, a producing method according to the present invention atleast includes a PL extracting step of extracting phospholipids (PL)from defatted cells obtained by extracting triglyceride (TG)-containingoil or fat from lipid producing cells.

That is, in the present invention, the defatted cells (residual cells)from which an oil or fat such as triglycerides has been removed are usedas a source of LCPUFA-PL. As such, the invention may include an oil orfat extracting step, carried out before the PL extracting step, ofextracting a TG-containing oil or fat from the lipid producing cells andobtaining defatted cells.

<Lipid Producing Cells>

The lipid producing cells used as a starting material in the presentinvention are not particularly limited as long as they aremicroorganisms capable of producing LCPUFA-PL. Specific examples includeMortierella, Conidiobolus, Pythium, Phytophthora, Penicillium,Cladosporium, Mucor, Fusarium, Aspergillus, Rhodotorula, Entomophthora,Echinosporangium, and Saprolegnia.

Lipid producing cells used as a starting material are selected accordingto the type of LCPUFA produced. For example, only one kind of strain maybe used, or two or more combinations of strains may be used.

Among these lipid producing cells, many species or strains ofMortierella are known to be capable of producing LCPUFA-PL that includesarachidonic acid (AA) as a constituent of LCPUFA (hereinafter AA-PL).When Mortierella are used, it is preferable that the cells belong tosubgenus Mortierella, examples of which include Mortierella alpina,Mortierella polycephala, Mortierella exigua, Mortierella hygrophila, andMortierella elongata.

More specifically, bacterial strains of subgenus Mortierella capable ofproducing AA-PL are, for example, M. polycephala IFO6335, M. elongataIFO8570, M. exigua IFO8571, M. hygrophila IFO5941, M. alpina IFO8568,ATCC16266, ATCC32221, ATCC42430, CBS219.35, CBS224.37, CBS250.53,CBS343.66, CBS527.72, CBS529.72, CBS608.70, and CBS754.68.

Other than subgenus Mortierella, the following strains are capable ofproducing AA-PL: Echinosporangium transversalis ATCC16960, Conidiobolusheterosporus CBS138.57, and Saprolegnia lapponica CBS284.38.

All of these strains are available from Institute for Fermentation,Osaka (IFO), American Type Culture Collection, ATCC, and Centrralbureauvoor Schimmelcultures (CBS), among others.

As another example of a strain of subgenus Mortierella capable ofproducing AA-PL, the strain M. elongata SAM0219 (International DepositNo. FERMBP-1239 based on Budapest Treaty), separated from soil by aresearch group including the inventors of the present invention, isavailable.

Further, a more specific example of microorganisms that belong tosubgenus Mortierella and is capable of producing LCPUFA-PL (DGLA-PL)whose LCPUFA constituent is dihomo-γ-linolenic acid (DGLA) is the strainM. elongata SAM1860 (International Deposit No. FERMBP-3589 based onBudapest Treaty) separated from soil by a research group including theinventors of the present invention.

Further, a more specific example of microorganisms that belong tosubgenus Mortierella and is capable of producing LCPUFA-PL (meadacid-PL) whose LCPUFA constituent is mead acid is the strain M. alpinaSAM2086 (International Deposit No. FERMBP-6032 based on Budapest Treaty)separated from soil by a research group including the inventors of thepresent invention.

<Culturing of Lipid Producing Cells>

The present invention is adapted to culture microorganisms (lipidproducing cells) capable of producing LCPUFA-PL, so as to produce thecells in a sufficient amount. As such, a producing method according tothe present invention may include a lipid producing cells culturing stepof culturing lipid producing cells.

A method of culturing the lipid producing cells is not specificallylimited, and a conventional method can be used depending on the type oflipid producing cells. Generally, a liquid medium or solid medium isinoculated with the spores or mycelia of lipid producing cells to becultured, or with a pre-culture solution of the lipid producing cells.When the cells are required in a large quantity, use of a liquid mediumis often more preferable. The culturing equipment is not particularlylimited. For a small culture, the cells may be cultured by shakingcultivation in a liquid medium placed in various types of test tubes orflasks, or by static cultivation by inoculating an agar plate. For alarge culture, various types of fermentors, including a jar fermentorcan be used.

The type of culture medium used is not particularly limited either, andis suitably selected and prepared from known components according to thetype of lipid producing cells used. Alternatively, a medium of a knowncomposition, or a commercially available medium can be used.

When a liquid medium is used, the carbon source is not particularlylimited and common sugars can be suitably used. Specific examples ofsuch sugars include glucose, fructose, xylose, saccharose, maltose,soluble starch, syrup, glycerol, and mannitol. These carbon sources canbe used either alone or in a combination of two or more kinds.

The nitrogen source is not particularly limited either, and conventionalsources can be suitably used. Some of the examples include: naturalsources such as peptone, yeast extract, malt extract, meat extract,cazamino acid, corn steep liquor, soybean protein, defatted soybean, andcotton seed lees; organic sources such as urea; and inorganic sourcessuch as sodium nitrate, ammonium nitrate, and ammonium sulfate. Amongthese examples, natural sources derived from soy beans are particularlysuitable in the present invention, though the type of suitable sourcevaries depending on the type of cultured strain.

Specific examples of such sources include soy beans, defatted soy beans,soy bean flakes, edible soy bean proteins, bean-curd refuse, soya milk,and soy flour. Among these examples, heat-denatured defatted soy beans,or more preferably defatted soy beans obtained by a heat treatment ofabout 70° C. to 90° C. and subsequent removal of an ethanol-solublecomponent can be used. These nitrogen sources can be used either aloneor in a combination of two or more kinds.

Components other than the carbon source or nitrogen source are notparticularly limited either. As required, a known mineral nutrientsource can be suitably selected and added. Examples of such nutrientsources include: ions of inorganic acid such as ions of phosphoric acid;ions of alkali metals or alkali earth metals, such as calcium ion,sodium ion, magnesium ion, and calcium ion; metal ions of groups VIIB toVIII, such as iron, nickel, cobalt, and manganese; metal ions of groupsIB to IIB, such as copper and zinc; and various vitamins.

The content (percent addition) of each component in a liquid medium isnot particularly limited, and a conventional amount can be suitablyadopted as long as it does not inhibit the growth of the lipid producingcells. In actual practice, the total amount of carbon source added ispreferably in a range of generally from 0.1 percent by weight to 40percent by weight, or more preferably 1 percent by weight to 25 percentby weight. In the case of a nitrogen source, the total amount added ispreferably in a range of generally from 0.01 percent by weight to 10percent by weight, or more preferably 0.1 percent by weight to 10percent by weight. In the case of a feeding culture, it is preferablethat the initial amount of carbon source added be in a range of 1percent by weight to 5 percent by weight, and that the initial amount ofnitrogen source added be in a range of 0.1 percent by weight to 6percent by weight. Both the carbon source and nitrogen source can be fedto the culture medium; however, it is more preferable to feed only thecarbon source.

Note that, in a producing method according to the present invention,precursors of unsaturated fatty acids can be added to the medium inorder to increase the yield of LCPUFA-containing unsaturated fattyacids. Non-limiting examples of the precursors of unsaturated fattyacids include: hydrocarbons such as hexadecane or octadecane; fattyacids or salts thereof, such as oleic acid or linoleic acid; fatty acidesters, such as ethylester, glycerine fatty acid ester, or sorbitanfatty acid ester; and oils or fats, such as olive oil, soy bean oil,rapeseed oil, cotton oil, and coconut oil. These precursors may be usedeither alone or in a combination of two or more kinds.

The amount of precursors of unsaturated fatty acids added is notparticularly limited. Generally, the precursors of unsaturated fattyacids are added in a range of 0.001 percent to 10 percent with respectto the total weight of the medium, or more preferably 0.5 percent to 10percent with respect to the total weight of the medium. The lipidproducing cells may be cultured using these precursors as a sole carbonsource.

The culture conditions are not particularly limited, and are suitablyselected according to the type of cultured strain. For example, theculture temperature is generally in a range of 5° C. to 40° C., or morepreferably 20° C. to 30° C. Alternatively, the cells may be grown firstin a temperature range of 20° C. to 30° C., and then 5° C. to 20° C.With such temperature control whereby cells are cultured first in arelatively high temperature range and then in a lower temperature range,the proportion of polyunsaturated fatty acids (PUFA) in the resultingunsaturated fatty acids can be increased.

The pH of the medium is not particularly limited either. Generally, a pHrange of 4 to 10 is used, or more preferably a pH range of 5 to 9 isused. The cultivation period is not particularly limited either.Generally, the cultivation period is 2 to 30 days, preferably 5 to 20days, and more preferably 5 to 15 days. The external process carried outon the medium is not particularly limited, and is suitably selected fromconventional cultivation methods, including stirring aerationcultivation, shaking cultivation, and static cultivation.

<Oil or Fat Extracting Step>

In the present invention, the PL extracting step is carried out aftercarrying out the oil or fat extracting step for the cells collected inthe lipid producing cell culturing step. The oil or fat extracting stepis for producing defatted cells (residual cells) from the collected massof cells, wherein an oil or fat such as triglycerides is extracted fromthe cells and removed. In this step, non-PL lipids are removed eitherentirely or partially without removing hardly any LCPUFA-PL. In otherwords, the oil or fat extracting step is the pre-step of the PLextracting step. It should be noted however that the oil or fat, such astriglycerides, extracted in the oil or fat extracting step containsLCPUFA as a constituent, and therefore has a good market value as aLCPUFA-containing oil or fat.

In the oil or fat extracting step, the collected cells may be usedeither directly as viable cells, or after sterilization. Further, thecells may be processed in the culture solution without being collected.Alternatively, the collected cells may be used either directly in theform of a cluster, or after they are processed into a plate, string,grain, powder, or any other form. The collecting method of cells is notparticularly limited either. When the amount of cultured cells is small,centrifugation can be carried out using a common centrifuge. On theother hand, when the amount of collected cells is large, it ispreferable that the cells be separated by continuous centrifugation,with or without filtration using a film, etc.

The collected cells may remain wet, or may be dried to obtain driedcells. In the present invention, use of dried cells is more preferable.In this way, an oil or fat can be efficiently extracted (see Examples).A method of drying the wet cells is not particularly limited. Forexample, conventional drying processes such as ventilation, a heattreatment, decompression, and lyophilization can be used.

Thus, after the lipid producing cell culturing step, a producing methodof the present invention may include a cell collecting step ofcollecting cells, and a cell processing step of processing the collectedcells. In the cell processing step, the collected cells may be processedinto an arbitrary form, or wet cells may be dried to obtain dried cells.

In the oil or fat extracting step, a method of extracting oil or fatfrom the cells is not particularly limited, and a conventionalextracting method can be used. Specifically, at least the followingmethods are available: compression extraction employing appliedpressure; rendering extraction using hot water or steam; and extractionusing various extractants.

The compression extraction employing applied pressure is notparticularly limited as long as it can extract an oil component in thecells by applying pressure on the material used. For example, a methodusing a hydraulic press of a batch type, or a method using devices suchas a continuous expeller can be used.

The rendering extraction is not particularly limited, and may be a drytype or wet type. Specifically, a dry type using direct fire, or steamrendering (wet type) by an autoclave are available.

To explain the dry type more specifically, oil or fat is liquated byheating the cells under direct fire or jacket steam, for example. Insteam rendering, specifically, the cells are exposed to heated steam. Byheating and stirring, the oil component is obtained in the form of anemulsion, along with other components such as water and protein. With acentrifuge, the waste water is separated, and a crude oil is obtainedwith optional filtration. The conditions of steam rendering are notparticularly limited. For example, elution may be carried out for 4 to 6hours under the heated steam of 3 kg/cm² to 4 kg/cm².

The type of extractant used for the extraction is not particularlylimited. Generally, an extract of at least one of an aliphatic organicsolvent and water is used. Alternatively, a supercritical carbon dioxidegas may be used. Among such extracts, specific examples of aliphaticorganic solvents include: saturated hydrocarbons such as hexane,petroleum ether (organic solvent including pentane and hexane as majorcomponents); ketones such as acetone; alcohols such as methanol,ethanol, propanol, and butanol; esters such as ethyl acetate; andhalogenated hydrocarbons such as chloroform and dichloromethane. In thecase of water, an aqueous solution dissolving a known solute may beused. These extracts may be used either alone or in a combination of twoor more kinds. Among the extracts as exemplified above, saturatedhydrocarbons such as hexane or petroleum ether are preferable, andhexane is more preferable, in order to efficiently remove oil or fatsuch as triglycerides.

The extraction process with the extractant may be carried out in a batchor continuously. The conditions of extraction with the extractant arenot particularly limited either. The temperature, the amount ofextractant used, and the time of extraction are suitably selectedaccording to the type of extracted oil or fat such as triglycerides, andthe amount of cells used (volume, weight). In the extraction, it ispreferable that the cells be gently stirred by being dispersed in theextractant. In this way, the extraction can be carried out efficiently.

Note that, after the oil or fat extracting step, the resulting defattedcells may be directly used in the PL extracting step, or may beprocessed and stored for later use. As described above, the oil or fatextracting step is one of the producing steps of defatted cells, as wellas a step of producing oil or fat, which itself has a market value.Thus, if the oil or fat is the required product, the defatted cells canbe regarded as a waste. In this case, the byproduct defatted cellsobtained in the production of oil or fat can be stored, and can be usedas a raw material in the production according to the present invention.As such, the oil or fat extracting step is not necessarily required inthe producing method of the present invention.

<PL Extracting Step>

In a producing method according to the present invention, the PLextracting step of extracting PL from defatted cells is essential. Inthe PL extracting step, the method of extracting PL from the defattedcells is not particularly limited. However, as in the oil or fatextracting step, it is preferable to use extraction with an extractant.

The extractant used to extract PL from the defatted cells is notparticularly limited. As in the oil or fat extracting step, an extractof at least one of an aliphatic organic solvent and water, orsupercritical carbon dioxide gas can be suitably used. Among suchextracts, examples of aliphatic organic solvents include: saturatedhydrocarbons such as hexane or petroleum ether (organic solventcontaining pentane and hexane as major components); ketones such asacetone; alcohols such as methanol, ethanol, propanol, and butanol;esters such as ethyl acetate; halogenated hydrocarbons such aschloroform and dichloromethane; cyanized hydrocarbons such asacetonitrile; and ethers such as diethyl ether. In the case of water, anaqueous solution dissolving a known solute may be used. These extractsmay be used either alone or in a combination of two or more kinds.

Among the extracts as exemplified above, preferable examples ofaliphatic organic solvents include: saturated hydrocarbons, alcohols, amixed solvent of saturated hydrocarbon and alcohol, and a mixed solventof halogenated hydrocarbon and alcohol. As a saturated hydrocarbon,hexane is preferable. As an alcohol, ethanol is preferable. As a mixedsolvent of saturated hydrocarbon and alcohol, a mixed solvent of hexaneand ethanol is preferable. As a mixed solvent of halogenated hydrocarbonand alcohol, a mixed solvent, of chloroform and methanol is preferable.

Among these organic solvents, hexane and/or ethanol are particularlypreferable when used in food. When using a mixture of hexane andethanol, it is preferable that the hexane:ethanol ratio of the mixturebe 4:1 to 0:6 by volume, more preferably 4:1 to 1:4 by volume, andfurther preferably 4:1 to 2:4 by volume. In the event where thehexane:ethanol ratio is 0:6, an organic solvent with 100% ethanol isused. When a mixed solvent of hexane and ethanol, or ethanol is used, asmall amount of water may be added.

The extraction process with the extractant may be carried out in a batchor continuously. The conditions of extraction with the extractant arenot particularly limited either. The temperature, the amount ofextractant used, and the time of extraction are suitably selectedaccording to the type of PL to obtain, and the amount of cells used(volume, weight). In the extraction, it is preferable that the cells begently stirred by being dispersed in the extractant. In this way, theextraction can be carried out efficiently.

<Other Steps>

As described above, a producing method according to the presentinvention at least includes the PL extracting step, and preferablyincludes the oil or fat extracting step. In addition, the method mayalso include other steps. Specific examples of such steps are the cellcollecting step and cell processing step, as described above. Further,as will be described in later Examples, a PL purifying step of purifyingthe PL obtained in the PL extracting step may be additionally included.

A specific method by which the PL purifying step is carried out, i.e., amethod of purifying the crude PL obtained in the PL extracting step isnot particularly limited. In later Examples, PL is purified by thinlayer chromatography (TLC). However, the method is not just limited tothis, and various solvent fractionating methods such as columnchromatography or acetone fractionation can be used. The carrier used inthe chromatography is not particularly limited, and conventionalcarriers can be suitably used. The solvent used in the solventfractionation is not particularly limited either, and conventionalsolvents can be suitably used.

<Phospholipids According to the Present Invention>

Phospholipids according to the present invention are produced by theproducing method described above. In other words, phospholipidsaccording to the present invention are extracted from the defatted cellsobtained by extracting TG-containing oil or fat from the lipid producingcells, and include LCPUFA as a constituent.

Phospholipids according to the present invention are not particularlylimited as long as they include LCPUFA as a constituent, and may be anyconventional phospholipids. Specific examples of such phospholipidsinclude: glycerophospholipids such as phosphatidylcholine (PC),phosphatidylserine (PS), phosphatidylethanolamine (PE),phosphatidylinositol (PI), phosphatidylglycerol (PG), and cardiolipin(CL); sphingophospholipids such as sphingomyelin (SP); andlysophospholipids such as lysophosphatidylcholine (LPC),lysophosphatidylserine (LPS), lysophosphatidylethanolamine (LPE),lysophosphatidylinositol (LPI), lysophosphatidylglycerol (LPG); andlysophospholipids such as phosphatidic acid. Among these phospholipids,PC, PS, PE, PI and phosphatidic acid are particularly preferable.

Phospholipids according to the present invention include at least onekind of phospholipids as exemplified above, and may include two or morekinds of phospholipids. In the case of crude phospholipids not purifiedby the purification step, various types of trace components may beadded. An example of such trace components is a lipid component (oil orfat, etc.) other than the phospholipids derived from the lipid producingcells.

The constituent LCPUFA of phospholipids according to the presentinvention is not particularly limited as long as it is an unsaturatedfatty acid having 20 or greater carbon atoms with a double bond.Specific examples of such unsaturated fatty acids include: eicosadienoicacid; eicosatrienoic acids such as dihomo-γ-linolenic acid and meadacid; eicosatetraenoic acids such as arachidonic acid (AA);eicosapentaenoic acid; docosadienoic acid; docosatrienoic acid;docosatetraenoic acid; docosapentaenoic acid; docosahexaenoic acid(DHA); tetracosadienoic acid; tetracosatrienoic acid;tetracosatetraenoic acid; tetracosapentaenoic acid; tetracosahexaenoicacid. Among these LCPUFA, arachidonic acid (AA) and/or docosahexaenoicacid (DHA) are preferable. Only one kind of LCPUFA, or two or more kindsof LCPUFA may be contained as constituents of the LCPUFA-PL.

In the LCPUFA, at least one of the C—C double bonds (—C═C—) in itsstructure may be conjugated. The conjugate double bonds may include acarbonyl group (C═O), or may be formed by adjacent C—C double bonds.

The proportion of LCPUFA with respect to total fatty acids contained inthe LCPUFA-PL is not particularly limited, but is preferably 22 percentby weight or greater, more preferably 31 percent by weight or greater,and further preferably 37 percent by weight or greater. When arachidonicacid (AA) is contained as LCPUFA, the proportion of AA with respect tototal fatty acids contained in the LCPUFA-PL is not particularlylimited, but is preferably 0.3 percent by weight or greater, morepreferably 5 percent by weight or greater, further preferably 20 percentby weight or greater, and particularly preferably 34 percent by weightor greater.

When the LCPUFA-PL is PC, the proportion of AA with respect to totalfatty acids contained as constituents of the total PC is preferably 15percent by weight or greater, or more preferably 40 percent or greater.When the LCPUFA-PL is PS, the proportion of AA with respect to totalfatty acids contained as constituents of the total PS is preferably 5percent by weight or greater, or more preferably 20 percent by weight orgreater. In this way, phospholipids according to the present inventioncan provide superior products such as nutritional compositions.

Note that, regardless of the producing method used, phospholipidsaccording to the present invention include LCPUFA-PL that contains atleast PC and PS, and LCPUFA that contains at least AA. In suchPC-PS-containing phospholipids with AA-containing LCPUFA, the proportionof AA with respect to total fatty acids contained as constituents of thetotal PC is 40 percent by weight or greater, and the proportion of AAwith respect to total fatty acids contained as constituents of the totalPS is 20 percent by weight or greater.

Further, phospholipids according to the present invention may include PCthat contains DGLA as LCPUFA, and may additionally include PS thatcontains DGLA as LCPUFA. When the phospholipids include PC that containsDGLA as LCPUFA, the proportion of DGLA with respect to total fatty acidscontained as constituents of the total PC is 3 percent by weight orgreater. When the phospholipids additionally include PS that containsDGLA as LCPUFA, the proportion of DGLA with respect to total fatty acidscontained as constituents of the total PS is 1 percent by weight orgreater.

The PC and PS behave differently in the body and have distinctphysiological functions. Thus, with the AA contained as LCPUFA, thecombined effects in the body make phospholipids of the present inventioneven more desirable as nutritional compositions. Further, with AA orDGLA contained as LCPUFA, the properties and functions of thesecompounds make phospholipids of the present invention even moredesirable as nutritional compositions.

The AA is one type of polyunsaturated fatty acid, and it constitutesabout 10 percent of fatty acids in the blood or an important organ suchas liver. More specifically, in the human blood, the composition ratiosof fatty acids in the phospholipids are 11 percent AA, 1 percenteicosapentaenoic acid (EPA), and 3 percent DHA. The AA is an importantconstituent of the cell membrane, and is involved in the regulation offluidity in the cell membrane. Various functions of AA in the bodymetabolism are known. It is also known that the AA serves as animportant direct precursor of prostaglandins.

Further, in recent years, the role of AA as a nutriment for infants hascaught the attention. The AA is also the subject of study as aconstituent fatty acid of endogenous cannabinoid (2-arachidonoylmonoglycerol, anandamide) that has neuroactive effects. Generally,ingestion of food rich in linoleic acid produces AA in the body throughconversion. However, in infants, elderly, and the patients or potentialpatients of common adult diseases, the catalytic action of enzymesinvolved in the biosynthesis of AA is weak, and the AA tends to bedeficient. Therefore, direct intake of AA is desired.

As with AA, the DGLA is also one type of polyunsaturated fatty acid, andit constitutes the fatty acids in the blood and important organs such asliver. In humans and other organisms, the composition ratio of DGLA isabout several percent with respect to total fatty acids. Further, aswith AA, the DGLA is also involved in the regulation of fluidity in thecell membrane. Various functions of DGLA in the body metabolism areknown. It is also known that the DGLA serves as an important directprecursor of prostaglandins. More specifically, it is known that series1 prostaglandins is produced from DGLA.

Particularly, various actions of series 1 prostaglandins produced fromDGLA have been under study, including, for example, platelet aggregatesuppressing action, vasodilating action, bronchodilating action, andanti-inflammatory action. Generally, DGLA is converted from linoleicacid. However, as with AA, DGLA becomes deficient when the activities ofenzymes involved in the DGLA biosynthesis are weak. Therefore, directintake is also desirable for DGLA.

As described above, phospholipids according to the present inventioninclude at least PC and PS as LCPUFA-PL, and additionally include atleast a certain amount of AA as a constituent of PC and PS. Thephospholipids of the invention are therefore highly desirable asnutritional compositions.

(II) Lipid Composition According to the Present Invention, and ProducingMethod Thereof

The composition, state, or other conditions of a lipid compositionaccording to the present invention are not particularly limited as longas the lipid composition includes phospholipids according to the presentinvention. In one preferable composition, at least LCPUFA-PL isdissolved as a solute in a liquid lipid used as a solvent, wherein theliquid lipid contain LCPUFA as a constituent (LCPUFA lipid). That is,one example of a lipid composition according to the present invention isa phospholipids solution in which LCPUFA-PL is dissolved in a liquidLCPUFA lipid.

<Absorption of LCPUFA-PL Contained in a Phospholipid Solution>

In a highly purified form, phospholipids exist as a powder, and isgenerally very hygroscopic and easily degradable (See BiochemistryExperiment Lecture 3, Science of Lipids, pp. 22-23, Tokyo Kagaku DojinCo., Ltd. (1974)). Therefore, for ease of handling, phospholipids areoften dissolved in a small amount of liquid lipid used as a solvent(phospholipid solution). As the liquid lipid used as a solvent,triglycerides (TG) etc. can be suitably used.

With the LCPUFA-PL prepared in a phospholipid solution, degradation ofLCPUFA-PL can be effectively prevented for better handling. However,when taken as food, efficient uptake of LCPUFA-PL is often prevented.Specifically, as described in the BACKGROUND ART section, thephospholipids in the digestive tract are absorbed in the form oflysophospholipids, and reassembled into phospholipids in the smallintestine. Here, when the phospholipids are ingested as a phospholipidssolution, the acyl group generated during the reassembly ofphospholipids from lysophospholipids includes both LCPUFA derived fromLCPUFA-PL, and fatty acids derived from the liquid lipid.

The TG generally used as the liquid lipid usually contain LCPUFA as aconstituent, but the concentration of LCPUFA is generally low. As such,the fatty acids providing the acyl group also include fatty acids otherthan LCPUFA (“non-LCPUFA fatty acids” hereinafter).

Thus, when the liquid lipid used as a solvent contain only a smallamount of LCPUFA, a large amount of non-LCPUFA fatty acid is used duringthe reassembly of phospholipids from lysophospholipids. As a result, theactual amount of absorbed LCPUFA-PL is greatly reduced even whenhigh-quality LCPUFA-PL is ingested as phospholipids.

It is therefore highly preferable that the liquid lipid be a LCPUFAlipid, such as TG, that contain a large amount of LCPUFA as aconstituent, because it allows the LCPUFA-PL to be efficiently absorbed.As such, the present invention is adapted to provide a lipid compositionin which the LCPUFA-PL is dissolved in a liquid LCPUFA lipid.

<Components of the Lipid Composition>

The liquid LCPUFA lipid used as a solvent of the phospholipids solutionare not particularly limited. For example, triglycerides, diglycerides,monoglycerides, fatty acids, and fatty acid alcohol ester can be used.Further, various types of LCPUFA described in the <Phospholipidsaccording to the present invention> section can be used as the LCPUFAcontained as a constituent of the LCPUFA lipid. Because the fatty acidscan be directly used as the LCPUFA lipid, the liquid LCPUFA themselvescan be used as the LCPUFA lipid.

As will be described later, TG-containing oil or fat obtained in the oilor fat extracting step of a producing method according to the presentinvention can be used as the LCPUFA lipid. The oil or fat, such astriglycerides, obtained by the oil or fat extracting step of the presentinvention can be suitably used as the LCPUFA oil or fat, because itcontains LCPUFA as a constituent.

The proportion of LCPUFA with respect to total fatty acids in the LCPUFAlipid is not particularly limited, but is preferably 11 percent byweight or greater, more preferably 25 percent or greater, and even morepreferably percent or greater. When arachidonic acid (AA) is containedas LCPUFA, the proportion of arachidonic acid with respect to totalfatty acids contained in the LCPUFA lipid is not particularly limited,but is preferably 9 percent by weight or greater, or more preferably 20percent or greater. The upper limit is not particularly limited butshould be as high as possible.

When the proportion of LCPUFA with respect to total fatty acids is inthese ranges, the LCPUFA content in the total fatty acids will notdecrease, or decreases only slightly, with respect to the lipidcomposition as a whole. In other words, the LCPUFA content in the liquidlipid which coexists with the LCPUFA-PL can be increased. In this way,when absorbed in the small intestine, a large amount of LCPUFA will beable to provide the acryl group during the reassembly of phospholipidsfrom the lysophospholipids. As a result, the amount of actually absorbedLCPUFA-PL will not decrease, or decreases only slightly.

The LCPUFA-PL is generally a powder, and is very hygroscopic and easilydegradable. However, by providing the LCPUFA-PL as a phospholipidsolution, it is not required to take into account these hygroscopic anddegradable properties of LCPUFA-PL. Further, with the LCPUFA-PL in theform of a liquid, overall handling can be further improved.

As the phospholipids used as a solute, phospholipids according to thepresent invention are used, i.e., phospholipids obtained by a producingmethod according to the present invention. However, in the presentinvention, a fat-soluble substance other than phospholipids may also beincluded as a solute.

Non-limiting examples of such fat-soluble substances include: sterols,sterol esters, glycolipids, sphingolipids, waxes, pigments, carotenoids,and tocopherols. A fat-soluble substance is suitably selected accordingto intended use of a lipid composition according to the presentinvention.

Various additives may be added to a lipid composition according to thepresent invention. Non-limiting examples of additives include: vitaminE, tocotrienol, sesamin, sesaminol, sesamol, astaxanthin, astaxanthinesters, sterols, and carotenes. Many of additives as exemplified aboveare already included in the fat-soluble composition. However, theadditives added to the fat-soluble composition are not necessarilyrequired to be fat soluble. A lipid composition according to the presentinvention can be used as a nutritional composition in food etc. As such,the invention can use all additives that can be added to food.

<Producing Method of the Lipid Composition>

A producing method of the lipid composition is not particularly limited.In the invention, phospholipids obtained by a producing method ofphospholipids according to the present invention are dissolved in liquidLCPUFA lipid, and optionally, other components are added and dissolvedor dispersed. In other words, a producing method of a lipid compositionaccording to the present invention at least includes the PL extractingstep, and also includes a solution preparing step of preparing aphospholipid solution by dissolving the PL-containing LCPUFA-PL obtainedin the PL extracting step in the LCPUFA lipid.

Further, in a lipid composition according to the present invention, theoil or fat obtained in the oil or fat extracting step can be suitablyused as the LCPUFA lipid. As such, a producing method of a lipidcomposition according to the present invention may include an oil or fatextracting step.

By controlling the procedure of extracting oil or fat such astriglycerides in the oil or fat extracting step, or the procedure ofextracting LCPUFA-PL in the PL extracting step, a lipid compositionaccording to the present invention can be produced more easily.Specifically, by suppressing the extent to which the oil or fat isremoved (extracted) from the lipid producing cells, the composition oflipids remaining in the resulting defatted cells can be varied.

The extent of removal is not particularly limited, and extractionconditions are suitably selected according to various prerequisites suchas the composition of the lipid composition, type of lipid producingcells, or the extraction method used to remove oil or fat from thecells. For example, when an aliphatic organic solvent is used as anextractant, conditions such as the amount of organic solvent, the numberof extraction processes, and extraction temperature are varied in theoil or fat extracting step. In this way, liquid oil or fat such astriglycerides (TG) can remain in the phospholipids obtained in the PLextracting step. Further, since the remaining liquid oil or fat is aLCPUFA lipid whose constituent is LCPUFA, a lipid composition can bereadily obtained. Thus, in the present invention, by suppressing theamount of extracted oil or fat in the oil or fat extracting step, alipid composition can be extracted as a phospholipid solution in the PLextracting step. In other words, the lipid composition as aphospholipids solution can be easily produced by varying conditions ofthe oil or fat extracting step in a producing method of phospholipidsaccording to the present invention.

In a lipid composition according to the present invention, the twoprimary components, LCPUFA-PL and LCPUFA lipid, can be mixed at anyproportions. As such, the amount of LCPUFA lipid is not particularlylimited as long as it can achieve the required fluidity for improvedhandling of the phospholipid solution.

Further, in order to adjust the concentrations of the primarycomponents, a lipid composition according to the present invention mayinclude lipids other than the lipids obtained by processes in aproducing method according to the present invention, i.e., the LCPUFA,or the oil or fat obtained from the lipid producing cells used as astarting material. As such lipids, any of LCPUFA-PL, non-LCPUFA, andLCPUFA lipid can be added.

Note that, a lipid composition according to the present invention is notjust limited to the phospholipid solution used for improved handling,and any other composition may be used. Further, since the lipidcomposition prepared as a phospholipid solution is dissolved mostly forimproved handling of the LCPUFA-PL, the lipid composition can bedirectly used as phospholipids.

(III) Use of the Present Invention

The use of the present invention is not particularly limited. As arepresentative example, phospholipids or a lipid composition accordingto the present invention can be used as a nutritional composition forsupplying LCPUFA-PL. The organism for which the nutritional compositionis used is not particularly limited. Human is a representative example.Other examples are domestic animals and test animals. The nutritionalcomposition may be ingested in any manner, but oral administration ismost preferable. Thus, the present invention includes food that includesthe phospholipids or lipid composition.

Food according to the present invention is not particularly limited aslong as phospholipids or a lipid composition according to the presentinvention is included. Non-limiting examples include: bread, sweets ofvarious kinds (including cold or frozen sweets), prepared food, dairyproducts, cereals, tofu, fried tofu, noodles, box lunch, seasonings,agricultural products such as wheat flour or meat, preserved food(canned food, frozen food, retort-packed food, etc.), soft drinks, milkbeverage, soy milk, soups such as potage soup, and all other commonfoods. A method by which the phospholipids or lipid composition areadded to these common foods is not particularly limited, and anyconventional method can be suitably used depending on the type of foodused.

Further, food according to the present invention includes functionalfoods used for specific purposes, such as health foods or nutriments.Specific examples include nutraceutical foods including varioussupplements, and specified health foods. For ease of handling, it ispreferable that phospholipids according to the present invention beprepared as a phospholipid solution. However, in the case ofsupplements, the phospholipid solution (lipid composition) can bedirectly used only by processing it into appropriate form. In this case,the form of the phospholipid solution is not particularly limited.Specifically, a lipid composition (or food) according to the presentinvention may be in the form of a liquid, powder, or capsule (seeExample 6 to be described later). Alternatively, a lipid compositionaccording to the present invention may be in the form of a pill ortablet. In using phospholipids or a lipid composition according to thepresent invention, all techniques such as dissolving in common oil- orfat-containing food, or powderization, applicable for common oil or fat,can be used.

Use of the present invention includes using phospholipids obtained bythe producing method. Thus, when phospholipids or a lipid compositionaccording to the present invention are used as food etc. with theaddition of other components, the additional components may besolubilized in the form of a liposome, using the phospholipids. In thiscase, a dispersion liquid of an oil-in-water (O/W) type with a liposomecan be used as a composition according to the present invention.

As described above, in the present invention, the LCPUFA-PL can beefficiently and stably obtained from the lipid producing cells obtainedby fermentation of microorganisms. Conventionally, animal organs such asthe cow brain have been the major source of LCPUFA-PL. However, with theepidemic of the mad cow disease, these conventional sources have beenavoided. The present invention, on the other hand, relies onfermentation techniques to obtain LCPUFA-PL. This is advantageous interms of customer acceptance, making the present invention particularlysuitable when the phospholipids or lipid composition are used in commonfoods or functional foods.

The applicable field of the invention is not just limited to food, butthe invention is also applicable in the field of medicine. That is,phospholipids or a lipid composition according to the present inventionmay also be used as medicines. In this case, the invention is not justlimited to a particular application, and any conventional technique maybe used depending on the intended use.

EXAMPLES

The following will describe the present invention in more detail basedon Examples. It is to be noted that the invention is not limited in anyway by the following Examples. The culture media used in the ProductionExamples 1 through 5 in producing dried cells and defatted cells aredescribed in detail in the following section “Preparation of CultureMedia.”

[Preparation of Culture Media]

The composition of seed culture medium A used in the Production Example1 for producing dried cells and defatted cells, was 1% yeast extract, 2%glucose, and the remaining being water. The media was adjusted to pH6.3. Similarly, the composition of seed culture medium B was 1% yeastextract, 2% glucose, 0.1% soy bean oil and the remaining being water.The media was adjusted to pH 6.3. For the main culture medium C, culturemedium C-b was added to culture medium C-a. The main culture medium Cwas prepared with pH 6.1. The culture medium C-a was prepared such that336 kg of a soy bean powder, 16.8 kg of KH₂PO₄, 2.8 kg of MgCl₂.6H₂O,2.8 kg of CaCl₂.2H₂O, and 56 kg of soy bean oil were added to water, andstirred. The solution was adjusted to 4500 L of final volume by addingwater, and subsequently was sterilized at 121° C. for 20 minutes. Theculture medium C-b was prepared such that 112 kg of hydrous glucose wasadded to water, and stirred. The solution was adjusted to 1000 L offinal volume by adding further water, and subsequently was sterilized at140° C. for 40 seconds.

The composition of the culture medium D used in the Production Examples2 through 5 for producing dried cells and defatted cells was 1.8%glucose, 1.5% soy bean powder, 0.1% soy bean oil, 0.3% KH₂PO₄, 0.1%Na₂SO₄, 0.05% CaCl₂.2H₂O, 0.05% MgCl₂.6H₂O, and the remaining beingwater. The culture medium D was adjusted to pH 6.3.

Production Example 1 for Producing Dried Cells and Defatted Cells

As the lipid-producing cells, Mortierella alpina CBS754.68 was used asone of the arachidonic acid-containing phospholipid producing cells. Astrain in custody of CBS754.68 was inoculated to the seed culture mediumA. The seed culture (the first step) started with shaking at 100 rpm and28° C. It was continued for three days. Subsequently 30 L of culturemedium B was prepared in an aerated stirring culture bath of 50 L. Tothe culture medium B, the seed culture (the first step) was inoculated.Seed culture (the second step) was started with stirring frequency of200 rpm and with the pressure in the bath of 150 kPa at 28° C. It wascontinued for 2 days.

Next, the seed culture (the second step) was inoculated to the mainculture medium C prepared up to 5600 L in the culture bath of 10 kLvolume. The main culture was started at a temperature of 26° C., withaerated volume of 49 Nm³/hr and with an internal pressure of 200 kPa.After an adequate time had passed, the culture feeding, in which anadequate amount of hydrous glucose was added, was suitably conducted. Asthe culture feeding, a total of 1454 kg of hydrous glucose was added sixtimes. Thus the main culture was continued for 306 hours.

After the main culture, the cells culture media were sterilized at 120°C. for 20 minutes, and then the wet cells were collected from the mediaby a hydro-extractor of continuous type. The wet cells were dried by afluidized-bed vibrating dryer so as to obtain dried cells dried up to 1%by weight of water. The dried cells were transported by a pneumatictransporter to a filling position, was filled with nitrogen gas into a 1m³ container bag made of aluminum pouch with its opening heat sealedafter the filling, and then stored in a refrigeration cabinet at 10° C.or below.

Three liter of hexane was added to 1 kg of the dried cells taken fromthe container bag. After the mixture was stirred gently at roomtemperature for 15 hours, the hexane layer was removed by filtration.From the obtained dried cells, residual hexane was removed by aerationso as to obtain the defatted cells A-1. To the defatted cells A-1, 3 Lof hexane was added again. After stirring gently for three hours at roomtemperature, and subsequent similar operation as the aforementionedoperation, the defatted cells A-2 were obtained.

After the second extraction process of hexane, 3 L of hexane was addedagain to the defatted cells A-2. After stirring gently for three hoursat room temperature, and subsequent similar operation as theaforementioned operation, the defatted cells A-3 were obtained. Again, 3L of hexane was added to the defatted cells A-3. After stirring gentlyfor three hours at room temperature, and subsequent similar operation asthe aforementioned operation, the defatted cells A-4 were obtained.

In the four extraction processes of hexane, the extracted lipid in anyof the collected hexane layers was almost exclusively triglycerides.Phospholipids were not detected in these layers.

Production Example 2 for Producing Dried Cells and Defatted Cells

Five liters of main culture medium D was prepared in a 10 L aeratedstirring culture bath and then sterilized. As lipid-producing cells,Mortierella polycephala IFO6335, a filamentous bacteria to producearachidonic acid, was inoculated and cultured at 26° C., with an aeratedvolume of 1 vvm and with the stirring frequency of 300 rpm. Theculturing was continued for 9 days. Depending on the consumption ofglucose, 1% glucose was suitably added. The cultured cells weresterilized in a similar manner as in the Example 1 and were dried afterthe culture medium was removed so as to obtain dried cells.

To 40 g of the dried cells, 120 mL of hexane was added. After themixture was stirred gently at room temperature for 3 hours, the hexanelayers were removed by filtration. Then, 120 mL of hexane was added tothe obtained cells again. After stirring gently for 15 hours at roomtemperature, the hexane layers were removed by filtration. From theobtained dried cells from which hexane was extracted, residual hexanewas removed by aeration so as to obtain the defatted cells B.

In the hexane layers collected in the extraction process of hexane, theextracted lipid was almost exclusively triglycerides. Phospholipids werenot detected in these layers.

Production Example 3 for Producing Dried Cells and Defatted Cells

Except that Mortierella elongata SAM1860 (International Deposit No.FERMBP-3589 based on Budapest Treaty), a filamentous bacteria to producedihomo-γ-linolenic acid (DGLA), was inoculated as lipid-producing cells,the similar procedure as in the Production Example 2 were conducted soas to obtain the defatted cells C.

In the hexane layers collected in the extraction process of hexane, theextracted lipid was almost exclusively triglycerides. Phospholipids werenot detected in these layers.

Production Example 4 for Producing Dried Cells and Defatted Cells

Except that Mortierella alpina SAM2086 (International Deposit No.FERMBP-15766 based on Budapest Treaty), filamentous bacteria to producemead acid, were inoculated as lipid-producing cells, a similar procedureas in the Production Example 2 was conducted so as to obtain thedefatted cells D.

In the hexane layers collected in the extraction process of hexane, theextracted lipid was almost exclusively triglycerides. Phospholipids werenot detected in these layers.

Production Example 5 for Producing Dried Cells and Defatted Cells

Except that Echinosporangium transversalis ATCC16960, filamentousbacteria to produce arachidonic acid, were inoculated as lipid-producingcells, a similar process as in the Production Example 2 was conducted soas to obtain the defatted cells E.

In the hexane layers collected in the extraction process of hexane, theextracted lipid was almost exclusively triglycerides. Phospholipids werenot detected in these layers.

Production Example 6 for Producing Dried Cells and Defatted Cells

Except that the culture time period was 6 days, a similar process as inthe Production Example 2 was conducted so as to obtain dried cellsMortierella polycephala IFO6335. In addition, except that the amount ofthe dried cells was 20 g and that the hexane volume was 60 mL, a similarprocess as in the Production Example 2 was conducted to obtain thedefatted cells F, Mortierella polycephala IFO6335.

In the hexane layers collected in the extraction process of hexane, theextracted lipid was almost exclusively triglycerides. Phospholipids werenot detected in these layers.

Production Example 7 for Producing Dried Cells and Defatted Cells

Except that the culture time period was 6 days, a similar process as inthe Production Example 5 was conducted to obtain dried cells ofEchinosporangium transversalis ATCC16960. In addition, except that theamount of the dried cells was 20 g and that the hexane volume was 60 mL,a similar process as in the Production Example 2 was conducted to obtainthe defatted cells G, Echinosporangium transversalis ATCC 16960.

In the hexane layers collected in the extraction process of hexane, theextracted lipid was almost exclusively triglycerides. Phospholipids werenot detected in these layers.

Example 1 Extraction of Phospholipids Containing Arachidonic Acid fromthe Defatted Cells A-2

Twenty five mL of various organic solvents were added as extractant toone gram of the defatted cells A-2 obtained in the Production Example 1for producing dried cells and defatted cells. The mixture was stirredgently at 60° C. for one hour. As an extraction media, hexane, mixedsolvents of hexane and ethanol (a to e), ethanol, a mixed solvent ofchloroform or methanol was used. The composition of these extractionmedia (mixing ratio by volume) is shown in Table 1.

TABLE 1 Compositions Extractant (mixing ratio by volume) HexaneHexane:Ethanol = 6:0 Mixed solvent of hexane and ethanol Hexane:Ethanol= 4:1 (a) Mixed solvent of hexane and ethanol Hexane:Ethanol = 4:2 (b)Mixed solvent of hexane and ethanol Hexane:Ethanol = 3:3 (c) Mixedsolvent of hexane and ethanol Hexane:Ethanol = 2:4 (d) Mixed solvent ofhexane and ethanol Hexane:Ethanol = 1:4 (e) Ethanol Hexane:Ethanol = 0:6Mixed solvent of chloroform and Chloroform:Methanol = 2:1 methanol

In either case, after the layers of the organic solvent were filtrated,collected and subsequently the organic solvent was removed so as toobtain a crude phospholipid fraction. The obtained phospholipid fractionwas fractionated into triglycerides (TG) and phospholipids (PL) bythin-layer chromatography with silica gel (TLC). A mixed solvent ofhexane and ethyl ether with the mixing ratio of 7:3 was used as adeveloping solvent. Both fractions were scratched and the fatty acidswere qualified and quantified by inducing the fractions toward methylester by way of methanol hydrochloride method. Pentadecanoic acid wasused as an internal reference. The result of the qualification andquantification of the fatty acids is shown in the Table 2.

TABLE 2 Lipids Content of as extracted LCPUFA in fatty acids (m/g totalfatty acids defatted cells) of PL Extractant PL TG AA DGLA Hexane 0.035.0 — — Mixed solvent of hexane and ethanol 20.0 40.0 43.0 2.6 (a)Mixed solvent of hexane and ethanol 24.4 40.4 43.7 2.5 (b) Mixed solventof hexane and ethanol 24.1 43.4 42.5 2.5 (c) Mixed solvent of hexane andethanol 19.9 45.2 42.7 2.6 (d) Mixed solvent of hexane and ethanol 16.441.8 42.5 2.6 (e) Ethanol 16.3 42.0 41.7 2.6 Mixed solvent of chloroformand 24.9 66.1 40.4 2.5 methanol

In the case where only hexane was used as extractant, the phospholipidswere not extracted. In other cases, on the other hand, a remarkableamount of phospholipids was extracted. In addition, not less than 40% ofthe total fatty acids in the phospholipids were LCPUFA such asarachidonic acid (AA) or dihomo-γ-linolenic acid (DGLA).Eicosapentaenoic acid (EPA), on the contrary, was not detected.

Example 2 Extraction of Phospholipids Containing Arachidonic Acid fromthe Defatted Cells A-1 Through A-4

One liter of a mixed solvent of hexane and ethanol (mixing ratio of 1:1by volume) was added to 200 grams of the defatted cells A-1 through A-4obtained in the Production Example 1 for producing dried cells anddefatted cells, respectively. The mixtures were stirred gently at 60° C.for 90 minutes. After filtration of the solvent layers, the sameoperation was repeated twice. All of the organic solvent layers werethen collected and removed so as to obtain a crude phospholipidfraction. The obtained phospholipid fraction were fractionated into TGand PL by thin-layer chromatography with silica gel (TLC), similarly asin the Example 1, so as to conduct qualification and quantification ofthe fatty acids. The result of the qualification and quantification isshown in Table 3. The weight in Table 3 indicates the amount per 1 g ofthe defatted cells.

TABLE 3 Content of Lipids as LCPUFA in total extracted fatty acids ineach LCPUFA in the Defatted fatty acids fraction (%) extracted lipids(mg) Defatted cells Fraction (mg) AA DGLA Total AA DGLA Total A-1 PL22.4 42.5 2.5 45.0 9.52 0.56 10.1 TG 98.3 42.0 2.5 44.5 41.3 2.46 43.8A-2 PL 23.0 42.5 2.6 45.1 9.78 0.60 10.4 TG 46.2 42.0 2.5 44.5 19.4 1.1620.6 A-3 PL 23.0 42.5 2.6 45.1 9.78 0.60 10.4 TG 26.8 41.8 2.5 44.3 11.20.67 11.9 A-4 PL 22.8 42.4 2.6 45.0 9.67 0.59 10.3 TG 19.7 40.9 2.5 43.48.06 0.49 8.55

The crude phospholipid fraction obtained from the defatted cells A-2 wasdissolved in cold acetone at 4° C., insoluble acetone constituent wascollected twice so as to obtain the purified phospholipid fraction. Thepurified phospholipid fraction did not contain neutral lipids. Inaddition, the ratio of AA and DGLA in the total fatty acid was 43.4% and2.6% respectively.

Further the purified phospholipid fraction was fractionated bythin-layer chromatography with silica (TLC) into phosphatidylcholine(PC), phosphatidylethanolamine (PE), phosphatidylserine (PS),phosphatidylinositol (PI) and glycolipids (GL), and then thequalification and quantification of the fatty acids were conducted. Amixed solvent of chloroform, methanol, acetic acids and water with themixing ratio of 100:75:7:4 was used as a developing solvent. Thecomposition of the obtained purified phospholipids is shown in Table 4.

TABLE 4 Content of LCPUFA in total fatty acids Percent by weight in eachfraction (%) Fraction as fatty acids (%) AA DGLA PC 58.9 53.7 3.1 PE25.1 33.9 1.7 PS 3.1 23.5 1.4 PI 5.4 22.2 3.3 GL 7.5 18.3 1.4

Example 3 Extraction of Phospholipids Containing PUFA from the DefattedCells B Through E

Twenty five mL of a mixed solvent of hexane and ethanol (mixing ratio of1:1 by volume) was added to 5 grams of the defatted cells B through Eobtained in the Production Examples 2 through 5 for producing driedcells and defatted cells, respectively. The mixtures were stirred gentlyat 60° C. for 90 minutes. After the layers of the organic solvent werefiltrated, the same operation was repeated twice. All of the layers ofthe organic solvent were then collected and removed so as to obtain acrude phospholipid fraction. The obtained phospholipids werefractionated, similarly as in Example 1, into TG and PL by thin-layerchromatography with silica gel (TLC) so as to conduct qualification andquantification of the fatty acids. The result of the qualification andquantification is shown in Table 5. The weight in Table 5 indicates theamount of the defatted cells per 1 g.

TABLE 5 Lipids as extracted Content of LCPUFA in total fatty fatty acidsin each fraction (%) LCPUFA in the acids Mead Total extracted lipidsDefatted cells Fraction (mg) AA DGLA acid LCPUFA (mg) B PL 20.0 20.2 2.30.0 22.5 4.50 TG 50.2 9.6 1.9 0.0 11.5 5.77 C PL 22.2 0.3 45.6 0.0 45.910.2 TG 43.0 0.0 35.7 0.0 35.7 15.4 D PL 22.3 0.0 0.0 31.1 31.1 6.94 TG42.0 0.0 0.0 25.8 25.8 10.8 E PL 21.5 34.7 3.1 0.0 37.8 8.13 TG 42.520.0 2.5 0.0 22.5 9.56

Example 4 Production of Purified LCPUFA-PL

Fifty mL of a mixed solvent of hexane and ethanol (mixing ratio of 1:1by volume) was added to 10 grams of the defatted cells F and G obtainedin the Production Examples 6 and 7 for producing dried cells anddefatted cells, respectively. The mixture was stirred gently at 60° C.for 90 minutes. After the solvent layers were filtrated, the sameoperation was repeated further twice. All of the solvent layers werethen collected and removed so as to obtain a crude phospholipidfraction. The obtained crude phospholipid fraction was dissolved in coldacetone at 4° C., and insoluble acetone constituent was collected twiceso as to obtain the purified phospholipid fraction. The purifiedphospholipid fraction did not contain neutral lipids. The purifiedphospholipid fraction was fractionated by a thin-layer chromatographywith silica gel (TLC) into phosphatidylcholine (PC),phosphatidylethanolamine (PE), phosphatidylserine (PS),phosphatidylinositol (PI) and glycolipids (GL), and then thequalification and quantification of the fatty acids were conducted. Amixed solvent of chloroform, methanol, acetic acids and water with themixing ratio of 100:75:7:4 was used as a developing solvent.

The composition of the purified phospholipids obtained from the defattedcells F is shown in Table 6, while the composition of the purifiedphospholipids obtained from the defatted cells G is shown in Table 7.

TABLE 6 Content of LCPUFA in total fatty acids Percent by weight in eachfraction (%) Fraction as fatty acids (%) AA DGLA PC 56.2 30.0 3.1 PE28.5 15.8 2.2 PS 10.2 15.6 1.1 PI 4.4 11.6 1.9 GL 0.7 8.5 1.3

TABLE 7 Content of LCPUFA in total fatty acids Percent by weight in eachfraction (%) Fraction as fatty acids (%) AA DGLA PC 60.2 17.9 2.1 PE23.1 10.0 1.7 PS 12.2 8.8 1.0 PI 3.2 9.5 0.9 GL 1.3 8.5 1.1

Example 5 Encapsulation with LCPUFA-Containing Phospholipids

A 100:35 mixture (weight ratio) of gelatin (Nitta Gelatin Inc.) andfood-additive glycerin (Kao Corporation) was prepared and water wasadded thereto. By dissolving the solution at 50° C. to 60° C., a gelatincoat with a viscosity of 2,000 cp was prepared.

Next, a crude phospholipid fraction, which was obtained from thedefatted cells A-2 in the Example 2, and a vitamin E oil (Eisai Co.,Ltd.) was mixed at a weight ratio of 100:0.05 so as to prepare theproduct 1.

Also a crude phospholipid fraction, which was obtained from the defattedcells A-2 in the Example 2, a purified phospholipid fraction extractedfrom salmon eggs (the ratio of DHA in the total fatty acids was 25%),soy bean oil (SHOWASANGYO Co., Ltd.) and a vitamin E oil (Eisai Co.,Ltd.) was mixed at a weight ratio of 50:50:50:0.05 so as to prepare theproduct 2.

By using the products 1 and 2, encapsulation and drying was conducted bya known method to produce a soft capsule containing 180 mg of theproduct pro grain. Either soft capsule was suitable for oral ingestion.

Example 6 Preparation of Drinks with LCPUFA-Containing Phospholipids

The crude phospholipid fraction, which was obtained from the defattedcells A-2 in the Example 2 was stirred in water at 60° C. for 5 to 30minutes, using a mixing-and-dispersing device (the Mtechnique product,CLEARMIX). As a result, a solution with dispersed liposome beinguniformly dispersed in water was obtained. The concentration ofphospholipids in the solution with dispersed liposome was from 0.1% to20% and was controllable freely.

The average grain diameter of liposome in the solution with dispersedliposome was from about 50 nm to about 100 nm. The solution withdispersed liposome containing 10% phospholipids was added to orangejuice, carbonated water, coffee, milk, soy milk, and a potage soup, eachin 1/100 (v/v), so as to prepare (produce) drinks as the food of thepresent invention. These drinks were suitable for oral ingestion.

The invention being thus described, it will be obvious that the same waymay be varied in many ways. Such variations were not to be regarded as adeparture from the spirit and scope of the invention, and all suchmodifications as would be obvious to one skilled in the art are intendedto be included within the scope of the following claims.

INDUSTRIAL APPLICABILITY

In a producing method of phospholipids according to the presentinvention, PL is extracted from defatted cells obtained by extractingoil or fat whose major component is TG from lipid producing cells, so asto efficiently produce LCPUFA-PL. The lipid producing cells can becultured for mass production, and therefore can be effectively used as asupply source.

Conventionally, the LCPUFA-PL are obtained only in a small quantity fromlimited sources, and as such the supply and quality of LCPUFA-PL areunstable. With the present invention, however, the LCPUFA-PL can bestably provided in a mass quantity and with a good quality. With theepidemics of various diseases such as the mad cow disease, use of animalorgans such as the cow brain has been practically impossible. It istherefore very meaningful, as in the present invention, to secure astable supply source of LCPUFA-PL that are safe to use.

The defatted cells are the by-product of the step in which oil or fatsuch as TG is extracted from cells. Conventionally, the defatted cellshave been disposed as a waste, or, at best, used as animal feedings, aswith residues of common microbial fermentation. The present invention,on the other hand, uses the defatted cells as the practical supplysource of LCPUFA-PL. The invention therefore enables the LCPUFA-PL to beproduced at relatively low cost, in addition to effectively using the“waste” defatted cells.

Phospholipids according to the present invention can be handled withease when provided as a solution using a liquid LCPUFA lipid as asolvent (lipid composition). Alternatively, the phospholipids can bedirectly used in food, so as to allow for efficient uptake of LCPUFA-PL.When the liquid LCPUFA lipid is oil or fat such as TG obtained in theoil or fat extracting step in particular, a high-quality lipidcomposition can be efficiently obtained.

The present invention therefore enables LCPUFA-PL to be produced bothefficiently and stably, and thereby provides LCPUFA-PL at low cost whileensuring stable supply and quality.

As described above, the present invention efficiently and stablyproduces LCPUFA-PL by fermentation techniques. The present invention istherefore applicable not only to industries dealing with functional foodbut also in industries dealing with food in general and even medicines.

1. A method for producing phospholipids that contain LCPUFA as aconstituent (LCPUFA-PL), wherein lipid producing cells producing lipidsthat contain long-chain polyunsaturated fatty acids (LCPUFA) asconstituents are used as a starting material, which comprises: (a) anoil or fat extracting step of extracting TG-containing oil or fat fromthe lipid producing cells and obtaining defatted cells; and (b) a PLextracting step of extracting phospholipids (PL) from the defatted cellsobtained in step (a), wherein a mixed solvent of hexane and ethanol isused as an extractant to extract PL from the defatted cells.
 2. Themethod as set forth in claim 1, wherein the lipid producing cells are atleast one kind selected from the group consisting of: Mortierella;Conidiobolus; Pythium; Phytophthora; Penicillium; Cladosporium; Mucor;Fusarium; Aspergillus; Rhodotorula; Entomophthora; Echinosporangium; andSaprolegnia.
 3. The method as set forth in claim 2, wherein the lipidproducing cells that belong to genus Mortierella also belong as subgenusMortierella.
 4. The method as set forth in claim 3, wherein the cellsthat belong to subgenus Mortierella are Mortierella alpina.
 5. Themethod as set forth in claim 1, wherein a hexane:ethanol ratio of themixed solvent of hexane and ethanol is in a range of 4:1 to 0:6 byvolume.
 6. The method as set forth in claim 1, wherein, in the oil orfat extracting step, the oil or fat is extracted from the lipidproducing cells using at least one of compression extraction employingapplied pressure, rendering extraction, and extraction using anextractant.
 7. The method as set forth in claim 6, wherein an extract ofat least one of an aliphatic organic solvent and water, or supercriticalcarbon dioxide gas is used as the extractant.
 8. The method as set forthin claim 7, wherein hexane is used as the aliphatic organic solvent. 9.The method as set forth in claim 1, wherein the lipid producing cellsused in the oil or fat extracting step are dried cells.
 10. The methodas set forth in claim 1, wherein a constituent LCPUFA in thephospholipid produced is at least one kind selected from the groupconsisting of: eicosadienoic acid, eicosatrienoic acid, eicosatetraenoicacid, eicosapentaenoic acid, docosadienoic acid, docosatrienoic acid,docosatetraenoic acid, docosapentaenoic acid, docosahexaenoic acid,tetracosadienoic acid, tetracosatrienoic acid, tetracosatetraenoic acid,tetracosapentaenoic acid, and tetracosahexaenoic acid.
 11. The method asset forth in claim 10, wherein at least one of C—C double bonds in aLCPUFA molecule is conjugated.
 12. The method as set forth in claim 10,wherein the LCPUFA includes arachidonic acid and/or docosahexaenoicacid.
 13. The method as set forth in claim 12, wherein a proportion ofarachidonic acid with respect to total fatty acids contained asconstituents of total LCPUFA-PL is 0.3 percent by weight or greater. 14.The method as set forth in claim 10, wherein the LCPUFA-PL is at leastone kind of glycerophospholipid selected from the group consisting of:phosphatidylcholine; phosphatidylserine; phosphatidylethanolamine;phosphatidylinositol; phosphatidic acid; and cardiolipin.
 15. The methodas set forth in claim 14, wherein the LCPUFA-PL is at leastphosphatidylcholine, and wherein a proportion of arachidonic acid withrespect to total fatty acids contained as constituents of totalphosphatidylcholine is 15 percent by weight or greater.
 16. The methodas set forth in claim 14, wherein the LCPUFA-PL is at leastphosphatidylserine, and wherein a proportion of arachidonic acid withrespect to total fatty acids contained as constituents of totalphosphatidylserine is 5 percent by weight or greater.
 17. A method ofproducing a lipid composition, comprising: a PL extracting step of themethod according to claim 1; and a solution preparing step of preparinga phospholipid solution by dissolving the LCPUFA-PL-containing PLobtained in the PL extracting step in a liquid lipid that contain LCPUFAas a constituent.
 18. The method as set forth in claim 17, furthercomprising an oil or fat extracting step, wherein oil or fat obtained inthe oil or fat extracting step is used as the liquid lipid.
 19. Themethod as set forth in claim 18, wherein an amount of oil or fatextracted in the oil or fat extracting step is suppressed, so as toextract in the PL extracting step the LCPUFA-PL as a lipid compositiondissolved in the liquid lipid.
 20. The method as set forth in claim 17,wherein a proportion of LCPUFA with respect to total fatty acids of theliquid lipid is 11 percent by weight or greater.